Modeling of gas-solid chemisorption in chemical heat pumps

被引:53
作者
Huang, HH
Wu, GB
Yang, J
Dai, YC [1 ]
Yuan, WK
Lu, HB
机构
[1] E China Univ Sci & Technol, UNILAB, Res Ctr Chem React Engn, Shanghai 200237, Peoples R China
[2] CNRS, Inst Sci & Genie Mat & Procedes, Lab Europeen Associe SIMAP, F-66860 Perpignan, France
基金
中国国家自然科学基金;
关键词
adsorption; ammonia; gas-solid reaction; refrigeration; sensitivity analysis; strontium chloride;
D O I
10.1016/S1383-5866(03)00192-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A model coupled the chemical kinetics with heat transfer was applied for simulation of the dynamic behavior of the gas-solid fixed-bed reactors used in chemical heat pumps (CHP). The kinetic parameters and the thermal parameters were identified, respectively. Good agreement was found between the simulation and the experimental data. Moreover, the sensitivity of the global advancements and the radial temperature profiles to the thermal parameters was analyzed. The thermal capacity of the reactive medium has little influence on the global advancement, while the effective thermal conductivity of the medium has an apparent effect on the global advancement. The influence of the effective thermal conductivity on the global advancement is significant until its value is larger than 15 W m(-1) K-1. The contact heat transfer coefficient between reactive salt and reactor wall has less influence on the global advancements and the radial temperature profiles when its value is higher than 800 W m(-2) K-1. This model can be used for optimal design of CHPs, optimization of the operation conditions, and determination of the influence of various parameters on the reactor performances, including the kinetic and thermal parameters, the operational parameters (imposed pressure and temperature), and the configuration parameters of the medium or reactor (geometry and dimensions). (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:191 / 200
页数:10
相关论文
共 12 条
[1]  
COSTE C, 1986, Patent No. 8309885
[2]  
Coste C, 1986, US Patent, Patent No. [4,595,774, 4595774]
[3]   A MODEL FOR REVERSIBLE SOLID GAS REACTIONS SUBMITTED TO TEMPERATURE AND PRESSURE CONSTRAINTS - SIMULATION OF THE RATE OF REACTION IN SOLID GAS REACTOR USED AS CHEMICAL HEAT-PUMP [J].
GOETZ, V ;
MARTY, A .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (17-18) :4445-4454
[4]   Testing and modelling of a temperature front solid-gas reactor applied to thermochemical transformer [J].
Goetz, V ;
Llobet, J .
APPLIED THERMAL ENGINEERING, 2000, 20 (02) :155-177
[5]   MODELS OF HEAT AND MASS TRANSFERS IN SOLID GAS REACTORS USED AS CHEMICAL HEAT-PUMPS [J].
LEBRUN, M ;
SPINNER, B .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (07) :1743-1753
[6]   Modelling of gas-solid reaction - Coupling of heat and mass transfer with chemical reaction [J].
Lu, HB ;
Mazet, N ;
Spinner, B .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (15) :3829-3845
[7]  
MAURAN S, 1991, Patent No. 910303
[8]   ANALYSIS AND EXPERIMENTAL-STUDY OF THE TRANSFORMATION OF A NONISOTHERMAL SOLID GAS REACTING MEDIUM [J].
MAZET, N ;
AMOUROUX, M ;
SPINNER, B .
CHEMICAL ENGINEERING COMMUNICATIONS, 1991, 99 :155-174
[9]   ANALYSIS OF HEAT-TRANSFER IN A NONISOTHERMAL SOLID-GAS REACTING MEDIUM [J].
MAZET, N ;
AMOUROUX, M .
CHEMICAL ENGINEERING COMMUNICATIONS, 1991, 99 :175-200
[10]   Development of a numerical sizing tool for a solid-gas thermochemical transformer .1. Impact of the microscopic process on the dynamic behaviour of a solid-gas reactor [J].
Neveu, P ;
CastaingLasvignottes, J .
APPLIED THERMAL ENGINEERING, 1997, 17 (06) :501-518